Ms. Loretta Barsamian May 23, 2001

Page 14

May 23, 2001 By email to James Nusrala and by mail

Ms. Loretta Barsamian, Executive Officer

Regional Water Quality Control Board

San Francisco Region

1515 Clay Street, Suite 1400

Oakland, CA 94612-1404

Attention: James Nusrala

Subject: City of San Mateo Final Effluent Limits Infeasibility Study

Dear Ms Barsamian:

INTRODUCTION

The following analysis of the feasibility of achieving compliance with projected final effluent limits for specific pollutants is provided for the City of San Mateo Wastewater Treatment Plant (WWTP).

BACKGROUND

The Policy for Implementation of Toxics Standards for Inland Surface Waters, Enclosed Bays and Estuaries of California (known as the State Implementation Policy (SIP)) establishes statewide policy for NPDES permitting. The SIP provides for the situation where an existing NPDES discharger cannot immediately comply with an effluent limitation derived from a California Toxics Rule (CTR) criterion. The SIP allows for the adoption of interim effluent limits and a schedule to come into compliance with the final limit in such cases. To qualify for interim limits and a compliance schedule, the SIP requires that an existing discharger demonstrate that it is infeasible to achieve immediate compliance with the CTR-based limit.

The term “infeasible” is defined in the SIP as “not capable of being accomplished in a successful manner within a reasonable period of time, taking into account economic, environmental, legal, social and technological factors.”

The SIP requires that the following information be submitted to the Regional Board to support a finding of infeasibility:

(a)  documentation that diligent efforts have been made to quantify pollutant levels in the discharge and sources of the pollutant in the waste stream, including the results of those efforts;

(b)  documentation of source control and/or pollution minimization efforts currently under way or completed;

(c)  a proposed schedule for additional or future source control measures, pollutant minimization or waste treatment; and

(d)  a demonstration that the proposed schedule is as short as practicable.

The SIP requires that interim numeric effluent limits be based on (a) current treatment facility performance or (b) limits in the existing permit, which ever is more stringent.

The SIP also requires that compliance schedules be limited to specific time periods, depending on whether the pollutant is on the 303(d) list. For pollutants not on the 303(d) list, the maximum length of the compliance schedule is 5 years from the date of permit issuance. For pollutants on the 303(d) list (where a TMDL is required to be prepared), the maximum length of the compliance schedule is 20 years from the effective date of the SIP (March 2000). To secure the TMDL-based compliance schedule, the discharger must make commitments to support and expedite development of the associated TMDL.

Four POTW NPDES permits are currently out for public review as Tentative Orders: Central Contra Costa Sanitary District (CCCSD), East Bay Municipal Utility District (EBMUD), Sewerage Agency of Southern Marin (SASM) and the City of San Mateo. These Tentative Orders include provisions for interim effluent limits and compliance schedules for selected pollutants which have been deemed to exhibit “reasonable potential” to cause or contribute to violations of water quality objectives. Regional Board staff has recently requested that information be submitted to demonstrate the need for interim limits and compliance schedules.

The following analysis pertains to the Tentative Order issued to San Mateo.

Pollutants to be Evaluated

The pollutants for which interim limits are proposed in the Tentative Order are as follows:

Copper

Mercury

Nickel

Cyanide

Tributyltin

Dieldrin

4,4-DDE

The feasibility of San Mateo achieving immediate and consistent compliance with final limits for these pollutants is evaluated below.

Final Limits

Regional Board staff has projected the following final effluent limits for the above pollutants. These values are taken from an undated document provided to dischargers by Regional Board staff on May 11, 2001. Values stated below are expressed as ug/l, unless otherwise noted. For this analysis, the projected final effluent values are taken at face value. The specific data, assumptions and calculations used in the determination of these final effluent values must be provided for review by the permittees before use in the NPDES permitting process. Verification of these values is not included in this analysis.

The proposed final average monthly effluent limits (AMEL) and maximum daily effluent limits (MDEL) shown below were calculated by RWQCB staff using procedures described in Section 1.4 of the SIP. Background values (maximum or average, as appropriate for the pollutant in question) were derived from Regional Monitoring Program data collected at two Central Bay stations (Yerba Buena Island and Richardson Bay). There are no background data for tributyltin. Dilution values used in the calculation of final effluent limits were as follows:

(1)  dilution = 10:1 for non-bioaccumulative pollutants (copper, nickel, and cyanide). Note that for cyanide, the dilution credit was eliminated because the ambient water concentration, based on very limited 1993 RMP data, was assumed equal to the water quality objective of 1.0 ug/l.

(2)  dilution = zero for 303(d) listed bioaccumulative pollutants (mercury, dieldrin, 4,4-DDE)

Other variables in the proposed final effluent limit calculations (all in ug/L) included coefficients of variation for different pollutants in different effluents, and freshwater versus saltwater objectives based on ambient salinity.

Pollutant AMEL MDEL

Copper 11.9 25.0

Nickel 29.5 71.1

Mercury 0.017 0.046

Cyanide 1 2

Tributyltin 0.067 0.135

Dieldrin 0.00014 0.00028

4,4-DDE 0.00059 0.00118

SAN MATEO WASTEWATER TREATMENT PLANT CAPACITY AND PERFORMANCE

The San Mateo wastewater treatment plant (WWTP) treats domestic and commercial wastewater from the City of San Mateo, the City of Foster City, the Town of Hillsborough, and portions of the City of Belmont and unincorporated San Mateo County (the Discharger’s service area). The wastewater collection system includes approximately 257 miles of sanitary sewer lines (gravity lines and force mains), and 23 pump stations. The flow from Foster City is via a separate forcemain with a separate flow meter. Foster City (Estero Municipal Improvement District) owns and maintains its own collection system and as such is a satellite collection system not regulated under the City’s NPDES permit.

The City currently (2001) serves a total population of approximately 136,600. There is limited growth projected for this primarily built out service area. The population is projected to increase by about four percent to approximately 141,040 by 2010. Non-residential development is projected to increase by about 10 percent from 7,183,000 square feet in 2001 to about 7,995,000 in 2010.

San Mateo presently discharges an average year-round flow of approximately 13.8 million gallons per day (mgd), and an average dry weather flow of 12.6 MGD from its advanced secondary treatment plant. The treatment plant has a current dry weather design capacity of 15.7 mgd and a peak wet weather flow capacity of approximately 40 mgd. San Mateo currently provides secondary treatment from October 1 until April 30 (the winter months) and when needed to meet conventional constituent effluent limits advanced secondary treatment from May 1 through September 30 (the summer months).

Treatment facilities consist of primary clarifiers, aeration tanks, final clarifiers, pressure filters (during the summer months), chlorination, and dechlorination. The treated wastewater is discharged into the deep water channel of lower San Francisco Bay, a water of the State and United States, at a point approximately 3,700 feet offshore and 500 feet north of the San Mateo-Hayward Bridge (Latitude 37 deg., 34 min., 50 sec.; longitude 122 deg., 14 min., 45 sec.) through a submerged diffuser at a depth of 41 feet below mean lower low water. The outfall is designed to provide an initial dilution of approximately 40:1 (ratio of receiving water to discharge).

The secondary plant and present solids handling processes went on line in 1978-79. In mid-to-late 1980's, plant staff converted existing storage tanks to first one, and then two, anaerobic digesters to treat the supernatant from the Zimpro high temperature, high pressure solids processing system.Additional improvements were added between 1992-1996 (Phase 1) to enhance solids handling capabilities and the ability to accommodate peak wet weather flows. The improvements included: improved headworks, a fifth aeration tank, a fifth secondary clarifier, a new expanded capacity effluent pump station, a dissolved air flotation thickener, an egg-shaped anaerobic digester, and improved sodium hypochlorite and sodium bisulfite handling facilities.

Sludge is thermally treated, dewatered using vacuum filters, and disposed of at the Richmond Landfill. The Discharger initiated its Phase II improvements in September 2000, consisting of a second anaerobic digester and new dewatering facilities to replace the existing Zimpro and vacuum filters solids processing system. This project is scheduled for completion in spring of 2003. Proposed Phase 3 improvements (projected for 2011) include one additional primary clarifier, one additional secondary clarifier, an additional digester, and potentially a recycled water package plant. All the currently scheduled improvements are intended to replace aging and outdated equipment to maintain overall plant reliability, not to expand plant hydraulic capacity, which will remain at the current 15.7 mgd.

PLANT PERFORMANCE AND FINAL EFFLUENT LIMIT ATTAINABILITY

Recent plant effluent quality (1998-2000) is summarized and compared with current and proposed final effluent limits in the attached table and time series line graphs. The feasibility of complying with RWQCB staff calculated SIP based limits is described below. The average monthly effluent limits (AMEL) are more stringent than the maximum daily effluent limits (MDEL). The AMEL is the controlling limit since effluent samples are generally only collected and analyzed monthly. The discussion below thus compares effluent quality with the AMEL.

A key infeasibility benchmark used here is comparison of the proposed final limits with the calculated interim performance based effluent limits (IPBL). IPBLs have typically been calculated as the mean plus three standard deviations of the last three years of log-transformed effluent data (IPBL calculations for each applicable constituent are attached). This approach has been adopted by RWQCB staff in part due to the SWRCB March 7, 2001 Tosco permit appeal final ruling directing the RWQCB to calculate interim limits in a representative manner that reflects the distribution of the underlying data. IBPLs calculated in this manner approximate the 99.87 percentile of plant performance (hereafter rounded to 99.9), a value that the plant would only be expected to exceed once every three years.

For purposes of this infeasibility study it is important to note that POTWs are designed to treat domestic wastewater and to remove conventional pollutants (i.e. TSS, BOD) not toxic pollutants. As stated in the Tentative Order (Footnote (1)(a) to Effluent Limitation 8) Toxic Substances),

Compliance with these limits shall be achieved through secondary treatment and, as necessary, pretreatment, source control, and pollution prevention.”

The 50 to 90% toxic pollutant removals typically achieved by secondary treatment plants are primarily attributable to effective suspended solids removal processes.

Copper

San Mateo could not comply with a final AMEL of 11.9 ug/L. The best estimation of recent plant performance is the IPBL, which is 33.1 ug/L. San Mateo would have violated the proposed AMEL if future conditions occurred similar to those in June 2000, May 1999, July 1998, and February 1998 when the measured effluent quality was 19, 12, 15, and 29 ug/L, respectively. Several other values from 1998-2000 were in the 10-11 ug/L range. San Mateo currently provides a consistently high level of advanced secondary treatment, as indicated by the average TSS concentration of about 10 mg/L, one-third of the standard 30 mg/L secondary treatment limit. As such there appears to be little room for improving potential compliance with trace metals limits (i.e. copper, nickel, and mercury) via further optimization of plant performance.

Nickel

It is not certain if San Mateo could consistently comply with a final AMEL of 29.5 ug/L. The best estimation of recent plant performance is the IPBL, which is 35.2 ug/L. As can be seen on the attached figure, although effluent concentrations have been below the proposed AMEL, the December 1998 value of 27 ug/L closely approached the AMEL. If that 27 ug/L value is deemed to be an outlier, and not representative of effluent quality, then it appears that San Mateo may be able to comply with the proposed AMEL. However, to date, RWQCB staff have not been amenable to excluding outlier values from RP and effluent limitation related analyses. San Mateo has been in consistent compliance with the current effluent limit of 65 ug/L.

Mercury

San Mateo could not comply with a final mercury AMEL of 0.017 ug/L. The best estimation of recent plant performance is the IPBL, which is 0.39 ug/L. San Mateo has been using ultraclean low detection limit analyses for mercury since before 1998 so that its dataset does not contain any high (e.g., 0.2 ug/L) non-detect values that complicate certain other treatment plant’s compliance evaluations. However, since the SIP states that interim limits should be set at the lower of the current permit limit or recent performance, the proposed interim limit defaults to the lower current permit limit value of 0.21 ug/L, which is almost 50% lower than the IPBL.

San Mateo would have frequently violated the proposed AMEL if future conditions occurred similar to those in 1998 and 1999. Even after initiating ultraclean sampling and analytical procedures in January 2000, San Mateo would have significantly exceeded the proposed AMEL based on January 2001 results (0.068 ug/L) and February 2001 results (0.026 ug/L). As can be seen in the attached figure, results from several other months in 2001 were also close to the proposed AMEL.

Cyanide

San Mateo could not comply with a final cyanide AMEL of 1.0 ug/L. Current analytical methodologies are unable to measure cyanide below 3 to 5 ug/L in wastewater effluent matrices. Therefore, it would be impossible to evaluate compliance with an AMEL set at 1.0 ug/L. It may also not be feasible to measure background receiving water concentrations at or below the WQO of 1.0 ug/L.

The best estimation of recent plant performance is the IPBL of 13 ug/L. However, since the SIP states that interim limits should be the lower of the current permit limit or recent performance, the proposed interim limit defaults to the lower current permit limit value of 10 ug/L. San Mateo has been in consistent compliance with that current permit limit, with most values reported as <5 ug/L. Cyanide has only been identified in the influent at detectable concentrations once (9.1 ug/L) in the past three years. The corresponding effluent concentration was only slightly above the detection limit (5.6 ug/L).